ular Snip Water-Rich Organic-Rich Overhead Phase Phase Phase Vapor Liquid Liquid Temperature, °C 76 40 40 Pressure, bar 1.4 1.4 1.4 Flow rate, kg/h: Isopropanol 6,800 5,870 930 Water 2,350 1,790 560 Benzene 24,600 30 24,570

Introduction to Chemical Engineering Thermodynamics
8th Edition
ISBN:9781259696527
Author:J.M. Smith Termodinamica en ingenieria quimica, Hendrick C Van Ness, Michael Abbott, Mark Swihart
Publisher:J.M. Smith Termodinamica en ingenieria quimica, Hendrick C Van Ness, Michael Abbott, Mark Swihart
Chapter1: Introduction
Section: Chapter Questions
Problem 1.1P
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Condenser duty for two-liquid-phase distillate.
Isopropanol, with 13 wt% water, can be dehydrated to obtain almost pure isopropanol at a 90% recovery by azeotropic distillation with benzene. When condensed, the overhead vapor from the column forms two immiscible liquid phases. Use Table 2.4 with data in Perry’s Handbook and the data below to compute the heat-transfer rate in Btu/h and kJ/h for the condenser.

ular Snip
Water-Rich
Organic-Rich
Overhead
Phase
Phase
Phase
Vapor
Liquid
Liquid
Temperature, °C
76
40
40
Pressure, bar
1.4
1.4
1.4
Flow rate, kg/h:
Isopropanol
6,800
5,870
930
Water
2,350
1,790
560
Benzene
24,600
30
24,570
Transcribed Image Text:ular Snip Water-Rich Organic-Rich Overhead Phase Phase Phase Vapor Liquid Liquid Temperature, °C 76 40 40 Pressure, bar 1.4 1.4 1.4 Flow rate, kg/h: Isopropanol 6,800 5,870 930 Water 2,350 1,790 560 Benzene 24,600 30 24,570
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